过程装备与控制工程专业英语翻译(2)
各专业英文翻译
法学 Law Study英语 English日语 Japanese信息与计算科学 Information and Computation Science应用物理学 Applied Physics冶金工程 Metallurgical Engineering金属材料工程 Metallic Materials Engineering无机非金属材料 Inorganic Nonmetallic Materials材料成型及控制工程 Material Formation and controlEngineering高分子材料与工程 Multimolecular Materials and Engineering工业设计 Industrial Disign建筑学 Architecture城市规划 City Planning艺术设计 Artistical Disign包装工程 Packaging Engineering机械设计制造及自动化Machine Disign,Manufacturing,and Automation热能与动力工程 Thermal and Power Engineering水利水电工程 WaterConservance and Electro-power Engineering测控技术与仪器 Technique and Instrumentation of Measurements电气工程及其自动化 Electric Engineering and its Automation自动化 Automation通信工程 Communication Engineering电子信息科学与技术 Sience and Technology of Electronic Information 计算机科学与技术 Computer Sience and Technology土木工程 Civil Engineering工程管理 Project Management给水排水工程 Water Supply and Sewage Engineering建筑环境与设备工程 Constructional Environment and Equipment Engineering 过程装备与控制工程 Processing Units and Control Engineering环境工程 Environmental Engineering化学工程与工艺 Chemacal Engineering and Technology平安工程 Safty Engineering工商管理 Industrial and Commercial Management市场营销 Market Management and Sales会计学 Accounting旅游管理 Tourism Management信息管理与信息系统 Information Management and System金融学 Finance国际经济与贸易 International Economy and Trade食品科学与工程 Food Sience and Engineering生物工程 Biological Engineering纺织工程 Textile Engineering建筑环境与设备工程、Constructional Environment and Equipment Engineering 过程装备与控制工程、Processing Units and Control Engineering现代家政学、 Modern Domestic Science运动训练科学系、 Sports Train Science食品营养与检测、 Food Nutrition and Detect国际新闻、 International News体育健康教育系 Sports Health Education哲学 Philosophy马克思主义哲学 Philosophy of Marxism中国哲学 Chinese Philosophy外国哲学 Foreign Philosophies逻辑学 Logic伦理学 Ethics美学 Aesthetics宗教学 Science of Religion科学技术哲学 Philosophy of Science and Technology经济学 Economics理论经济学 Theoretical Economics政治经济学 Political Economy经济思想史 History of Economic Thought经济史 History of Economic西方经济学 Western Economics世界经济 World Economics人口、资源与环境经济学 Population, Resources and Environmental Economics应用经济学 Applied Economics国民经济学 National Economics区域经济学 Regional Economics财政学〔含税收学〕 Public Finance (including Taxation)金融学〔含保险学〕 Finance (including Insurance)产业经济学 Industrial Economics国际贸易学 International Trade劳动经济学 Labor Economics统计学 Statistics数量经济学 Quantitative Economics中文学科、专业名称英文学科、专业名称国防经济学 National Defense Economics法学 Law法学 Science of Law法学理论 Jurisprudence法律史 Legal History宪法学与行政法学 Constitutional Law and Administrative Law 刑法学 Criminal Jurisprudence民商法学(含劳动法学、社会保障法学) Civil Law and Commercial Law (including Science of Labour Law and Science of Social Security Law )诉讼法学 Science of Procedure Laws经济法学 Science of Economic Law环境与资源保护法学 Science of Environment and Natural Resources Protection Law国际法学(含国际公法学、国际私法学、国际经济法学、) International law (including International Public law, International Private Law and International Economic Law)军事法学 Science of Military Law政治学 Political Science政治学理论 Political Theory中外政治制度 Chinese and Foreign Political Institution科学社会主义与国际共产主义运动 Scientific Socialism and InternationalCommunist Movement中*史(含党的学说与党的建设) History of the Communist Party of China(including the Doctrine of China Party and Party Building) 马克思主义理论与思想政治教育 Education of Marxist Theory and Education in Ideology and Politics国际政治学 International Politics国际关系学 International Relations外交学 Diplomacy社会学 Sociology社会学 Sociology人口学 Demography人类学 Anthropology民俗学(含中国民间文学) Folklore (including Chinese Folk Literature)民族学 Ethnology民族学 Ethnology马克思主义民族理论与政策 Marxist Ethnic Theory and Policy 中国少数民族经济 Chinese Ethnic Economics中国少数民族史 Chinese Ethnic History中国少数民族艺术 Chinese Ethnic Art教育学 Education教育学 Education Science教育学原理 Educational Principle课程与教学论 Curriculum and Teaching Methodology教育史 History of Education比拟教育学 Comparative Education学前教育学 Pre-school Education高等教育学 Higher Education成人教育学 Adult Education职业技术教育学 Vocational and Technical Education特殊教育学 Special Education教育技术学 Education Technology心理学 Psychology根底心理学 Basic Psychology开展与心理学 Developmental and Educational Psychology应用心理学 Applied Psychology体育学 Science of Physical Culture and Sports体育人文社会学 Humane and Sociological Science of Sports 运动人体科学 Human Movement Science体育教育训练学 Theory of Sports Pedagogy and Training民族传统体育学 Science of Ethnic Traditional Sports文学 Literature中国语言文学 Chinese Literature文艺学 Theory of Literature and Art语言学及应用语言学 Linguistics and Applied Linguistics汉语言文字学 Chinese Philology中国古典文献学 Study of Chinese Classical Text中国古代文学 Ancient Chinese Literature中国现当代文学 Modern and Contemporary Chinese Literature 中国少数民族语言文学 Chinese Ethnic Language and Literature比拟文学与世界文学 Comparative Literature and World Literature外国语言文学 Foreign Languages and Literatures英语语言文学 English Language and Literature俄语语言文学 Russian Language and Literature法语语言文学 French Language and Literature德语语言文学 German Language and Literature日语语言文学 Japanese Language and Literature印度语言文学 Indian Language and Literature西班牙语语言文学 Spanish Language and Literature阿拉伯语语言文学 Arabic Language and Literature欧洲语言文学 European Language and Literature亚非语言文学 Asian-African Language and Literature外国语言学及应用语言学 Linguistics and Applied Linguistics in Foreign Languages新闻传播学 Journalism and Communication新闻学 Journalism传播学 Communication艺术学 Art艺术学 Art Theory音乐学 Music美术学 Fine Arts设计艺术学 Artistic Design戏剧戏曲学 Theater and Chinese Traditional Opera电影学 Film播送电视艺术学 Radio and television Art舞蹈学 Dance历史学 History历史学 History史学理论及史学史 Historical Theories and History of Historical Science考古学及博物馆学 Archaeology and Museology历史地理学 Historical Geography历史文献学(含敦煌学、古文字学) Studies of Historical Literature (includingPaleography and Studies of Dunhuang)专门史 History of Particular Subjects中国古代史 Ancient Chinese History中国近现代史 Modern and Contemporary Chinese History世界史 World History理学 Natural Science数学 Mathematics根底数学 Fundamental Mathematics计算数学 Computational Mathematics概率论与数理统计 Probability and Mathematical Statistics 应用数学 Applied mathematics运筹学与控制论 Operational Research and Cybernetics物理学 Physics理论物理 Theoretical Physics粒子物理与原子核物理 Particle Physics and Nuclear Physics原子与分子物理 Atomic and Molecular Physics等离子体物理 Plasma Physics凝聚态物理 Condensed Matter Physics声学 Acoustics光学 Optics无线电物理 Radio Physics化学 Chemistry无机化学 Inorganic Chemistry分析化学 Analytical Chemistry有机化学 Organic Chemistry物理化学〔含化学物理〕 Physical Chemistry (including Chemical Physics)高分子化学与物理 Chemistry and Physics of Polymers天文学 Astronomy天体物理 Astrophysics天体测量与天体力学 Astrometry and Celestial Mechanics地理学 Geography自然地理学 Physical Geography人文地理学 Human Geography地图学与地理信息系统 Cartography and Geography Information System大气科学 Atmospheric Sciences气象学 Meteorology大气物理学与大气环境 Atmospheric Physics and Atmospheric Environment海洋科学 Marine Sciences物理海洋学 Physical Oceanography海洋化学 Marine Chemistry海洋生理学 Marine Biology海洋地质学 Marine Geology地球物理学 Geophysics固体地球物理学 Solid Earth Physics空间物理学 Space Physics地质学 Geology矿物学、岩石学、矿床学 Mineralogy, Petrology, Mineral Deposit Geology地球化学 Geochemistry古生物学与地层学〔含古人类学〕 Paleontology and Stratigraphy (including Paleoanthropology)构造地质学 Structural Geology第四纪地质学 Quaternary Geology生物学 Biology植物学 Botany动物学 Zoology生理学 Physiology水生生物学 Hydrobiology微生物学 Microbiology神经生物学 Neurobiology遗传学 Genetics发育生物学 Developmental Biology细胞生物学 Cell Biology生物化学与分子生物学 Biochemistry and Molecular Biology 生物物理学 Biophysics生态学 Ecology系统科学 Systems Science系统理论 Systems Theory系统分析与集成 Systems Analysis and Integration科学技术史 History of Science and Technology工学 Engineering力学 Mechanics一般力学与力学根底 General and Fundamental Mechanics固体力学 Solid Mechanics流体力学 Fluid Mechanics工程力学 Engineering Mechanics机械工程 Mechanical Engineering机械制造及其自动化 Mechanical Manufacture and Automation 机械电子工程 Mechatronic Engineering机械设计与理论 Mechanical Design and Theory车辆工程 Vehicle Engineering光学工程 Optical Engineering仪器科学与技术 Instrument Science and Technology精密仪器及机械 Precision Instrument and Machinery测试计量技术及仪器 Measuring and Testing Technologies and Instruments材料科学与工程 Materials Science and Engineering材料物理与化学 Materials Physics and Chemistry材料学 Materialogy材料加工工程 Materials Processing Engineering冶金工程 Metallurgical Engineering冶金物理化学 Physical Chemistry of Metallurgy钢铁冶金 Ferrous Metallurgy有色金属冶金 Non-ferrous Metallurgy动力工程及工程热物理 Power Engineering and Engineering Thermophysics工程热物理 Engineering Thermophysics热能工程 Thermal Power Engineering动力机械及工程 Power Machinery and Engineering流体机械及工程 Fluid Machinery and Engineering制冷及低温工程 Refrigeration and Cryogenic Engineering化工过程机械 Chemical Process Equipment电气工程 Electrical Engineering电机与电器 Electric Machines and Electric Apparatus电力系统及其自动化 Power System and its Automation高电压与绝缘技术 High Voltage and Insulation Technology 电力电子与电力传动 Power Electronics and Power Drives电工理论与新技术 Theory and New Technology of Electrical Engineering电子科学与技术 Electronics Science and Technology物理电子学 Physical Electronics电路与系统 Circuits and Systems微电子学与固体电子学 Microelectronics and Solid State Electronics电磁场与微波技术 Electromagnetic Field and Microwave Technology信息与通信工程 Information and Communication Engineering 通信与信息系统 Communication and Information Systems信号与信息处理 Signal and Information Processing控制科学与工程 Control Science and Engineering控制理论与控制工程 Control Theory and Control Engineering检测技术与自动化装置 Detection Technology and Automatic Equipment系统工程 Systems Engineering模式识别与智能系统 Pattern Recognition and Intelligent Systems导航、制导与控制 Navigation, Guidance and Control计算机科学与技术 Computer Science and Technology计算机软件与理论 Computer Software and Theory计算机系统结构 Computer Systems Organization计算机应用技术 Computer Applied Technology建筑学 Architecture建筑历史与理论 Architectural History and Theory建筑设计及其理论 Architectural Design and Theory城市规划与设计〔含风景园林规划与设计〕 Urban Planning and Design (including Landscape Planning and Design)建筑技术科学 Building Technology Science土木工程 Civil Engineering岩土工程 Geotechnical Engineering结构工程 Structural Engineering市政工程 Municipal Engineering供热、供燃气、通风及空调工程 Heating, Gas Supply, Ventilating and Air Conditioning Engineering防灾减灾工程及防护工程 Disaster Prevention and Reduction Engineering and Protective Engineering桥梁与隧道工程 Bridge and Tunnel Engineering水利工程 Hydraulic Engineering水文学及水资源 Hydrology and Water Resources水力学及河流动力学 Hydraulics and River Dynamics水工结构工程 Hydraulic Structure Engineering水利水电工程 Hydraulic and Hydro-Power Engineering港口、海岸及近海工程 Harbor, Coastal and Offshore Engineering 测绘科学与技术 Surveying and Mapping大地测量学与测量工程 Geodesy and Survey Engineering摄影测量与遥感 Photogrammetry and Remote Sensing地图制图学与地理信息工程 Cartography and Geographic Information Engineering化学工程与技术 Chemical Engineering and Technology化学工程 Chemical Engineering化学工艺 Chemical Technology生物化工 Biochemical Engineering应用化学 Applied Chemistry工业催化 Industrial Catalysis地质资源与地质工程 Geological Resources and Geological Engineering矿产普查与勘探 Mineral Resource Prospecting and Exploration 地球探测与信息技术 Geodetection and Information Technology 地质工程 Geological Engineering矿业工程 Mineral Engineering采矿工程 Mining Engineering矿物加工工程 Mineral Processing Engineering平安技术及工程 Safety Technology and Engineering石油与天然气工程 Oil and Natural Gas Engineering油气井工程 Oil-Gas Well Engineering油气田开发工程 Oil-Gas Field Development Engineering油气储运工程 Oil-Gas Storage and Transportation Engineering 纺织科学与工程 Textile Science and Engineering纺织工程 Textile Engineering纺织材料与纺织品设计 Textile Material and Textiles Design纺织化学与染整工程 Textile Chemistry and Dyeing and Finishing Engineering服装设计与工程 Clothing Design and Engineering轻工技术与工程 The Light Industry Technology and Engineering 制浆造纸工程 Pulp and Paper Engineering制糖工程 Sugar Engineering发酵工程 Fermentation Engineering皮革化学与工程 Leather Chemistry and Engineering交通运输工程 Communication and Transportation Engineering道路与铁道工程 Highway and Railway Engineering交通信息工程及控制 Traffic Information Engineering & Control 交通运输规划与管理 Transportation Planning and Management载运工具运用工程 Vehicle Operation Engineering船舶与海洋工程 Naval Architecture and Ocean Engineering船舶与海洋结构物设计制造 Design and Construction of Naval Architecture and Ocean Structure轮机工程 Marine Engine Engineering水声工程 Underwater Acoustics Engineering航空宇航科学与技术 Aeronautical and Astronautical Science and Technology飞行器设计 Flight Vehicle Design航空宇航推进理论与工程 Aerospace Propulsion Theory and Engineering航空宇航器制造工程 Manufacturing Engineering of Aerospace Vehicle人机与环境工程 Man-Machine and Environmental Engineering兵器科学与技术 Armament Science and Technology武器系统与运用工程 Weapon Systems and Utilization Engineering 兵器发射理论与技术 Armament Launch Theory and Technology火炮、自动武器与弹药工程 Artillery, Automatic Gun and Ammunition Engineering军事化学与烟火技术 Military Chemistry and Pyrotechnics核科学与技术 Nuclear Science and Technology核能科学与工程 Nuclear Energy Science and Engineering核燃料循环与材料 Nuclear Fuel Cycle and Materials核技术及应用 Nuclear Technology and Applications辐射防护及环境保护 Radiation and Environmental Protection农业工程 Agricultural Engineering农业机械化工程 Agricultural Mechanization Engineering农业水土工程 Agricultural Water-Soil Engineering农业生物环境与能源工程 Agricultural Biological Environmental and Energy Engineering农业电气化与自动化 Agricultural Electrification and Automation林业工程 Forestry Engineering森林工程 Forest Engineering木材科学与技术 Wood Science and Technology林产化学加工工程 Chemical Processing Engineering of Forest Products环境科学与工程 Environmental Science and Engineering环境科学 Environmental Science环境工程 Environmental Engineering生物医学工程 Biomedical Engineering食品科学与工程 Food Science and Engineering食品科学 Food Science粮食、油脂及植物蛋白工程 Cereals, Oils and Vegetable Protein Engineering农产品加工及贮藏工程 Processing and Storage of Agriculture Products水产品加工及贮藏工程 Processing and Storage of Aquatic Products农学 Agriculture作物学 Crop Science作物栽培学与耕作学 Crop Cultivation and Farming System作物遗传育种学 Crop Genetics and Breeding园艺学 Horticulture果树学 Pomology蔬菜学 Olericulture茶学 Tea Science农业资源利用学 Utilization Science of Agricultural Resources 土壤学 Soil Science植物营养学 Plant Nutrition植物保护学 Plant Protection植物病理学 Plant Pathology农业昆虫与害虫防治 Agricultural Entomology and Pest Control 农药学 Pesticide Science畜牧学 Animal Science动物遗传育种与繁殖 Animal Genetics, Breeding and Reproduction Science动物营养与饲料科学 Animal Nutrition and Feed Science草业科学 Practaculture Science特种经济动物饲养学〔含蚕、蜂等〕 The Rearing of Special-type EconomicAnimals (including Silkworm, Honeybees, etc.)兽医学 Veterinary Medicine根底兽医学 Basic Veterinary Medicine预防兽医学 Preventive Veterinary Medicine临床兽医学 Clinical Veterinary Medicine林学 Forestry林木遗传育种学 Forest Tree Genetics and Breeding森林培育学 Silviculture森林保护学 Forest Protection森林经理学 Forest Management野生动植物保护与利用 Wildlife Conservation and Utilization 园林植物与欣赏园艺 Ornamental Plants and Horticulture水土保持与荒漠化防治 Soil and Water Conservation and Desertification Combating水产学 Fisheries Science水产养殖学 Aquaculture Science捕捞学 Fishing Science渔业资源学 Science of Fisheries Resources医学 Medicine根底医学 Basic Medicine人体解剖与组织胚胎学 Human Anatomy, Histology and Embryology 免疫学 Immunology病原生物学 Pathogenic Organisms病理学与病理生理学 Pathology and Pathophysiology法医学 Forensic Medicine放射医学 Radiation Medicine航空航天与航海医学 Aerospace and Nautical medicine临床医学 Clinical Medicine内科学〔含心血管病学、血液病学、呼吸系病学、消化系病学、内分泌与代谢病学、肾脏病学、风湿病学、传染病学〕 Internal medicine (including Cardiology, Hematology, Respiratory, Gastroenterology, Endocrinology and Metabolism, Nephrology, Rheuma-tology, Infectious Diseases)儿科学 Pediatrics老年医学 Geriatrics神经病学 Neurology精神病与精神卫生学 Psychiatry and Mental Health皮肤病与性病学 Dermatology and Venereology影像医学与核医学 Imaging and Nuclear Medicine临床检验诊断学 Clinical Laboratory Diagnostics护理学 Nursing外科学〔含普通外科学、骨外科学、泌尿外科学、胸心血管外科学、神经外科学、整形外科学、烧伤外科学、野战外科学〕 Surgery (General Surgery, Orthopedics, Urology, Cardiothoracic Surgery, Neurosurgery, Plastic Surgery, Burn Surgery, Field Surgery)妇产科学 Obstetrics and Gynecology眼科学 Ophthalmic Specialty耳鼻咽喉科学 Otolaryngology肿瘤学 Oncology康复医学与理疗学 Rehabilitation Medicine & Physical Therapy 运动医学 Sports Medicine麻醉学 Anesthesiology急诊医学 Emergency Medicine口腔医学 Stomatology口腔根底医学 Basic Science of Stomatology口腔临床医学 Clinical Science of Stomatology公共卫生与预防医学 Public Health and Preventive Medicine 流行病与卫生统计学 Epidemiology and Health Statistics劳动卫生与环境卫生学 Occupational and Environmental Health 营养与食品卫生学 Nutrition and Food Hygiene儿少卫生与妇幼保健学 Maternal, Child and Adolescent Health 卫生毒理学 Hygiene Toxicology军事预防医学 Military Preventive Medicine中医学 Chinese Medicine中医根底理论 Basic Theories of Chinese Medicine中医临床根底 Clinical Foundation of Chinese Medicine中医医史文献 History and Literature of Chinese Medicine方剂学 Formulas of Chinese Medicine中医诊断学 Diagnostics of Chinese Medicine中医内科学 Chinese Internal Medicine中医外科学 Surgery of Chinese Medicine中医骨伤科学 Orthopedics of Chinese Medicine中医妇科学 Gynecology of Chinese Medicine中医儿科学 Pediatrics of Chinese Medicine中医五官科学 Ophthalmology and Otolaryngoloy of Chinese Medicine针灸推拿学 Acupuncture and Moxibustion and Tuina of Chinese medicine民族医学 Ethnomedicine中西医结合医学 Chinese and Western Integrative Medicine中西医结合根底医学 Basic Discipline of Chinese and Western Integrative中西医结合临床医学 Clinical Discipline of Chinese and Western Integrative Medicine药学 Pharmaceutical Science药物化学 Medicinal Chemistry药剂学 Pharmaceutics生药学 Pharmacognosy药物分析学 Pharmaceutical Analysis微生物与生化药学 Microbial and Biochemical Pharmacy药理学 Pharmacology中药学 Science of Chinese Pharmacology军事学 Military Science军事思想学及军事历史学 Military Thought and Military History 军事思想学 Military Thought军事历史学 Military History战略学 Science of Strategy军事战略学 Military Strategy战争发动学 War Mobilization战役学 Science of Operations联合战役学 Joint Operation军种战役学〔含第二炮兵战役学〕 Armed Service Operation (including Operation of Strategic Missile Force)战术学 Science of Tactics合同战术学 Combined-Arms Tactics兵种战术学 Branch Tactics军队指挥学 Science of Command作战指挥学 Combat Command军事运筹学 Military Operation Research军事通信学 Military Communication军事情报学 Military Intelligence密码学 Cryptography军事教育训练学〔含军事体育学〕 Military Education and Training (including Military Physical Training)军制学 Science of Military System军事组织编制学 Military Organizational System军队管理学 Military Management军队政治工作学 Science of Military Political Work军事后勤学与军事装备学 Science of Military Logistics and Military Equipment军事后勤学 Military Logistics前方专业勤务 Rear Special Service军事装备学 Military Equipment管理学 Management Science管理科学与工程 Management Science and Engineering工商管理学 Science of Business Administration会计学 Accounting企业管理学〔含财务管理、市场营销学、人力资源管理学〕 Corporate Management (including Financial Management, Marketing, and Human Resources Management)旅游管理学 Tourist Management技术经济及管理学 Technology Economy and Management农林经济管理学 Agricultural and Forestry Economics & Management农业经济管理学 Agricultural Economics & Management林业经济管理学 Forestry Economics & Management公共管理学 Science of Public Management行政管理学 Administration Management社会医学与卫生事业管理学 Social Medicine and Health Management教育经济与管理学 Educational Economy and Management社会保障学 Social Security土地资源管理学 Land Resource Management图书馆、情报与档案学 Science of Library, Information and Archival图书馆学 Library Science情报学 Information Science档案学 Archival Science。
过程装备与控制工程相关书籍
过程装备与控制工程相关书籍
与过程装备与控制工程相关的书籍有《过程设备与工业应用丛书》。
该丛书共6个分册，包括《反应过程、设备与工业应用》、《燃烧技术、设备与工业应用》、《传热技术、设备与工业应用》、《输送技术、设备与工业应用》、《分离技术、设备与工业应用》和《工业过程设备维护与检修》。
此外，还有《过程装备与控制工程专业基础课教程》等书籍，这些书籍涵盖了过程装备与控制工程的相关知识，有助于读者深入了解该领域。
请注意，这些书籍可能存在一定的局限性，为了获取更全面和准确的信息，建议读者查阅相关领域的专业书籍或者咨询专业人士。
新疆大学各个学院各个专业的英语翻译
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过程装备与控制工程专业英语翻译14
Reading material 14Evaporation1． IntroductionThe objective of evaporation is to concentrate a solution consisting of a nonvolatile solute and a volatile solvent. In the overwhelming majority of evaporations the solvent is water. Evaporation is conducted by vaporizing a portion of the solvent to produce a concentrated solution of thick liquor. Evaporation differs from drying in that the residue is a liquid-sometimes is highly viscous one-rather than a solid; it differs from distillation in that the vapor usually is a single component, and even when the vapor is a mixture, no attempt is made in the evaporation step to separate the vapor into fractions; it differs from crystallization in that emphasis is placed on concentrating a solution rather than forming and building crystals. In certain situations, e.g., in the evaporation of brine to produce common salt, the line between evaporation and crystallization is far from sharp. Evaporation sometimes produces a slurry of crystal in a saturated mother liquor.Normally, in evaporation the thick liquor is the valuable product and the vapor is condensed and discarded. In one specific situation, however, the reverse is true. Mineral-bearing water often is evaporated to give a solid-free product for boiler feed, for special process requirements, or for human consumption. This technique is often called water distillation, but technically it is evaporation. Large-scale evaporation processes have been developed and used for recovering potable water from seawater. Here the condensed water is the desired product. Only a fraction of the total water in the feed is recovered, and the remainder is returned to the sea.2. Liquid CharacteristicsThe practical solution of an evaporation problem is profoundly affected by the character of the liquor to be concentrated. It is the wide variation in liquor characteristics (which demands judgment and experience in designing and operating evaporators) that broadens this operation from simple heat transfer to a separate art. Some of the most important properties of evaporating liquids are as follows. Concentration Although the thin liquor fed to an evaporator may be sufficiently dilute to have many of the physical of water, as the concentration increases, the solution becomes more and more individualistic. The density and viscosity increase with solid content until either the solution becomes saturated or the liquor becomes too viscous for adequate heat transfer. Continued boiling of a saturated solution causes crystals to form; these must be removed or the tubes clog. The boiling point of the solution may also rise considerably as the solid content increases, so that the boiling temperature of a concentrated solution may be much higher than that of water at the same pressure.FoamingSome materials, especially organic substances, foam during vaporization. A stable foam accompanies the vapor out of the evaporator, causing heavy entertainment. In the extreme cases, the entire mass of liquid may boil over into the vapor outletand be lost.Temperature sensitivity Many fine chemicals pharmaceutical products, and foods are damaged when heated to moderate temperatures for relatively short times. In concentrating such materials special techniques are needed to reduce both the temperature of the liquid and the time of heating.Scale Some solutions deposit scale on the heating surface. The overall coefficient then steadily diminished, until the evaporator must be shut down and the tubes cleaned. When the scale is hard and insoluble, the cleaning is difficult and expensive.Materials of construction Whenever possible, evaporator are made of some kind of steel. Many solutions, however, attack ferrous metals or are contaminated by them. Special materials such as copper, nickel, stainless steel, aluminum, imperious graphite, and lead are then used. Since these materials are expensive, high heat transfer rates become especially desired to minimize the first cost of the equipment. Many other liquid characteristics must be considered by the designer of an evaporator. Some of these are specific heat, heat of concentration, freezing point, gas liberation on boiling, toxicity, explosion hazards, radioactivity, and necessity for sterile operation. Because of the variation in liquor properties, many different evaporator designers have been developed. The choice for any specific problem depends primarily on the characteristics of the liquid.3. Single and multiple-effect operationMost evaporators are heated by steam condensing on the metal tubes. Nearly always the material to be evaporated flows inside the tubes. Usually the steam is at low pressure, below 3 atm abs; often the boiling liquid is under moderate vacuum, at pressure down to about 0.05 atm abs. Reducing the boiling temperature of the liquid increase the temperature difference between the steam and the boiling liquid and thus increase the heat transfer rate in the evaporator.When a single evaporator is used, the vapor from the boiling liquid is condensed and discarded. This method is called single-effect evaporation, and although it is simple, it utilizes steam ineffectively. To evaporate 1 kg water from a solution call for from 1 to 1.3 kg of steam. If the vapor from one evaporator is fed into steam chest of a second evaporator and the vapor from second is then sent to a condenser, the operation becomes double-effect. The heat in the original steam is reused in the second effect, and the evaporation achieved by a unit mass of steam fed to the first effect is approximately doubled. Additional effects can be added in the same manner. The general method of increasing the evaporation per kilogram of steam by using a series of evaporator between the steam supply and the condenser is called multiple-effect evaporation.4. General types of evaporatorHorizontal-tube natural circulation evaporator the horizontal bundle of heating tubes is similar to the bundle of tubes in a heat exchanger. The steam enters into the tubes, where it condenses. The steam condensate leaves at the other end of the tubes. The boiling liquid solution covers the tubes. The vapor leaves the liquid surface, often goes through some deentraining device such as a baffle to preventcarryover of liquid droplets, and leaves out the top. This type is relatively cheap and is used for no viscous liquid having high heat transfer coefficients and liquids that do not deposit scale. Since liquid circulation is poor, they are unsuitable for viscous liquid. In almost all cases, this evaporator and the types discussed below are operating continuously, where the feed enters at a constant rate and the concentrate leaves at a concentrate rate.Vertical-type natural circulation evaporator in this type of evaporator, vertical rather than horizontal tubes are used, and the liquid is inside the tubes and the steam condenses outside the tubes. Because of boiling and decreases in density, the liquid rises in the tubes by natural circulation and flows downward through a large central open space or downcomer. This natural circulation increases the heat transfer coefficient. It is not used with viscous liquid. This type is often called the short-tube evaporator. A variation of this is the basket type. Where vertical tubes are used, but the heating element is held suspended in the body so there is an annular open space as the downcomer. The basket type differs from the vertical natural circulation evaporator, which has a central instead of annular open space as the downcomer, this type is widely used in the sugar, salt, and caustic soda industries.Long-tube vertical-type evaporator since the heat transfer coefficient on the steam side is very high compared to that on the evaporating liquid side, high liquid velocities are desirable. In a long-tube vertical-type evaporator the liquid is inside the tubes. The tubes are 3 to 10 m long and the formation of vapor bubbles inside the tubes causes a pumping action giving quite high liquid velocities. Generally, the liquid passes through the tubes only once and is not reticulated. Contact times can be quite low in this type. In some case,as when the ratio of the feed to evaporation rate is low.Natural recirculation of the product through the evaporators done by adding a large pipe connection between the outlet concentrate line and the feed line. This is widely used for producing condensed milk. Falling-film evaporator a variation of the long tube type is the falling-film evaporator, wherein the liquid is fed to the top of the tubes and flows down the walls as a thin film. Vapor-liquid separation usually takes place at the bottom. This type is widely used for concentrating heat-sensitive material such as orange juice and the other fruit juices, because the holdup time is very small (5 to 10 s or more).and the heat-transfer coefficients are high.Forced-circulation type evaporator this liquid film heat transfer coefficient can be increased by pumping to cause forced circulation of the liquid inside the tubes. This could be done in the long tube vertical type by adding a pipe concentrate with a pump between the outlet concentrate line and the feed line. However, usually in a forced-circulation type, the vertical tubes are shorter than in the long-tube type. Also, in other cases a separate and external horizontal heat exchanger is used. This type is very useful for viscous liquids.阅读材料14蒸发1、介绍蒸发的目的是浓缩不易挥发的溶质和易挥发的溶剂组成的溶液。
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过程装备与控制工程专业U形管换热器毕业论文外文文献翻译及原文
毕业设计（论文）外文文献翻译文献、资料中文题目：U形管换热器文献、资料英文题目：文献、资料来源：文献、资料发表（出版）日期：院（部）：专业：过程装备与控制工程专业班级：姓名：学号：指导教师：翻译日期： 2017.02.14毕业设计（论文）外文翻译毕业设计（论文）题目： U形管式换热器设计外文题目： U-tube heat exchangers译文题目：指导教师评阅意见U-tube heat exchangersM. Spiga and G. Spiga, Bologna1 Summary:Some analytical solutions are provided to predict the steady temperature distributions of both fluids in U-tube heat exchangers. The energy equations are solved assuming that the fluids remain unmixed and single-phased. The analytical predictions are compared with the design data and the numerical results concerning the heat exchanger of a spent nuclear fuel pool plant, assuming distinctly full mixing and no mixing conditions for the secondary fluid (shell side). The investigation is carried out by studying the influence of all the usual dimensionless parameters (flow capacitance ratio, heat transfer resistance ratio and number of transfer units), to get an immediate and significant insight into the thermal behaviour of the heat Exchanger.More detailed and accurate studies about the knowledge of the fluid temperature distribution inside heat exchangers are greatly required nowadays. This is needed to provide correct evaluation of thermal and structural performances, mainly in the industrial fields (such as nuclear engineering) where larger, more efficient and reliable units are sought, and where a good thermal design can not leave integrity and safety requirements out of consideration [1--3]. In this view, the huge amount of scientific and technical informations available in several texts [4, 5], mainly concerning charts and maps useful for exit temperatures and effectiveness considerations, are not quite satisfactory for a more rigorous and local analysis. In fact the investigation of the thermomechanieal behaviour (thermal stresses, plasticity, creep, fracture mechanics) of tubes, plates, fins and structural components in the heat exchanger insists on the temperature distribution. So it should be very useful to equip the stress analysis codes for heat exchangers withsimple analytical expressions for the temperature map (without resorting to time consuming numerical solutions for the thermal problem), allowing a sensible saving in computer costs. Analytical predictions provide the thermal map of a heat exchanger, aiding in the designoptimization.Moreover they greatly reduce the need of scale model testing (generally prohibitively expensive in nuclear engineering), and furnish an accurate benchmark for the validation of more refined numerical solutions obtained by computer codes. The purpose of this paper is to present the local bulk-wall and fluid temperature distributions forU-tube heat exchangers, solving analytically the energy balance equations.122 General assumptionsLet m, c, h, and A denote mass flow rate (kg/s), specific heat (J/kg -1 K-l), heat transfer coefficient(Wm -2 K-l), and heat transfer surface (m2) for each leg, respectively. The theoretical analysis is based on classical assumptions [6] :-- steady state working conditions,-- equal flow distribution (same mass flow rate for every tube of the bundle),-- single phase fluid flow,-- constant physical properties of exchanger core and fluids,-- adiabatic exchanger shell or shroud,-- no heat conduction in the axial direction,-- constant thermal conductances hA comprehending wall resistance and fouling.According to this last assumption, the wall temperature is the same for the primary and secondary flow. However the heat transfer balance between the fluids is quite respected, since the fluid-wall conductances are appropriately reduced to account for the wall thermal resistance and thefouling factor [6]. The dimensionless parameters typical of the heat transfer phenomena between the fluids arethe flow capacitance and the heat transfer resistance ratiosand the number of transfer units, commonly labaled NTU in the literature,where (mc)min stands for the smaller of the two values (mc)sand (mc)p.In (1) the subscripts s and p refer to secondary and primary fluid, respectively. Only three of the previous five numbers are independent, in fact :The boundary conditions are the inlet temperatures of both fluids3 Parallel and counter flow solutionsThe well known monodimensional solutions for single-pass parallel and counterflow heat exchanger,which will be useful later for the analysis of U-tube heat exchangers, are presented below. If t, T,νare wall, primary fluid, and secondary fluid bulk temperatures (K), and ξ and L represent the longitudinal space coordinate and the heat exchanger length (m), the energy balance equations in dimensionless coordinate x = ξ/L, for parallel and counterflow respectivelyread asM. Spiga and G. Spiga: Temperature profiles in U-tube heat exchangersAfter some algebra, a second order differential equation is deduced for the temperature of the primary (or secondary) fluid, leading to the solutionwhere the integration constants follow from the boundary conditions T(0)=T i , ν(0)≒νifor parallel T(1) = Ti ,ν(0) = νifor counter flow. They are given-- for parallel flow by - for counterflow byWishing to give prominence to the number of transfer units, it can be noticed thatFor counterflow heat exchangers, when E = 1, the solutions (5), (6) degenerate and the fluidtemperatures are given byIt can be realized that (5) -(9) actually depend only on the two parametersE, NTU. However a formalism involving the numbers E, Ns. R has been chosen here in order to avoid the double formalism (E ≤1 and E > 1) connected to NTU.4 U-tube heat exchangerIn the primary side of the U-tube heat exchanger, whose schematic drawing is shown in Fig. 1, the hot fluid enters the inlet plenum flowing inside the tubes, and exits from the outlet plenum. In the secondary side the fluid flows in the tube bundle (shell side). This arrangement suggests that the heat exchanger can be considered as formed by the coupling of a parallel and a counter-flow heat exchanger, each with a heigth equal to the half length of the mean U-tube. However it is necessary to take into account the interactions in the secondary fluid between the hot and the cold leg, considering that the two flows are not physically separated. Two extreme opposite conditions can be investigated: no mixing and full mixing in the two streams of the secondary fluid. The actual heat transfer phenomena are certainly characterized by only a partial mixing ofthe shell side fluid between the legs, hence the analysis of these two extreme theoretical conditions will provide an upper and a lower limit for the actual temperature distribution.4.1 No mixing conditionsIn this hypothesis the U-tube heat exchanger can be modelled by two independent heat exchangers, a cocurrent heat exchanger for the hot leg and a eountercurrent heat exchanger for the cold leg. The only coupling condition is that, for the primary fluid, the inlet temperature in the cold side must be the exit temperature of the hot side. The numbers R, E, N, NTU can have different values for the two legs, because of thedifferent values of the heat transfer coefficients and physical properties. The energy balance equations are the same given in (2)--(4), where now the numbers E and Ns must be changed in E/2 and 2Ns in both legs, if we want to use in their definition the total secondary mass flow rate, since it is reduced in every leg to half the inlet mass flow rate ms. Of course it is understood that the area A to be used here is half of the total exchange area of the unit, as it occurs for the length L too. Recalling (5)--(9) and resorting to the subscripts c and h to label the cold and hot leg, respectively, the temperature profile is given bywhere the integration constants are:M. Spiga and G. Spiga: Temperature profiles in U-tube heat exchangersIf E, = 2 the solutions (13), (14) for the cold leg degenerate into4.2 Full mixing conditionsA different approach can be proposed to predict the temperature distributions in the core wall and fluids of the U-tube heat exchanger. The assumption of full mixing implies that the temperaturesof the secondary fluid in the two legs, at the same longitudinal section, are exactly coinciding. In this situation the steady state energy balance equations constitute the following differential set :The bulk wall temperature in both sides is thenand (18)--(22) are simplified to a set of three equations, whose summation gives a differential equation for the secondary fluid temperature, withgeneral solutionwhere # is an integration constant to be specified. Consequently a second order differential equation is deduced for the primary fluid temperature in the hot leg :where the numbers B, C and D are defined asThe solution to (24) allows to determine the temperaturesand the number G is defined asThe boundary conditions for the fluids i.e. provide the integration constantsAgain the fluid temperatures depend only on the numbers E and NTU.5 ResultsThe analytical solutions allow to deduce useful informations about temperature profiles and effectiveness. Concerning the U-tube heat exchanger, the solutions (10)--(15) and (25)--(27) have been used as a benchmark for the numerical predictions of a computer code [7], already validated, obtaining a very satisfactory agreement.M. Spiga and G. Spiga: Temperature profiles in U-tube heat exchangers 163 Moreover a testing has been performed considering a Shutte & Koerting Co. U-tube heat exchanger, designed for the cooling system of a spent nuclear fuel storage pool. The demineralized water of the fuel pit flows inside the tubes, the raw water in the shell side. The correct determination of the thermal resistances is very important to get a reliable prediction ; for every leg the heat transfer coefficients have been evaluated by the Bittus-Boelter correlation in the tube side [8], by the Weisman correlation in the shell side [9] ; the wall material isstainless steel AISI 304.and the circles indicate the experimental data supplied by the manufacturer. The numbers E, NTU, R for the hot and the cold leg are respectively 1.010, 0.389, 0.502 and 1.011, 0.38~, 0.520. The difference between the experimental datum and the analytical prediction of the exit temperature is 0.7％ for the primary fluid, 0.9% for the secondary fluid. The average exit temperature of the secondary fluid in the no mixing model differs from the full mixing result only by 0.6%. It is worth pointing out the relatively small differences between the profiles obtained through the two different hypotheses (full and no mixing conditions), mainly for the primary fluid; the actual temperature distribution is certainly bounded between these upper and lower limits,hence it is very well specified. Figures 3-5 report the longitudinal temperaturedistribution in the core wall, τw = (t -- νi)/(Ti -- νi), emphasizing theeffects of the parameters E, NTU, R.As above discussed this profile can be very useful for detailed stress analysis, for instance as anM. Spiga and G. Spiga: Temperature profiles in U-tube heat exchangersinput for related computer codes. In particular the thermal conditions at the U-bend transitions are responsible of a relative movement between the hot and the cold leg, producing hoop stresses with possible occurrence of tube cracking . It is evident that the cold leg is more constrained than the hot leg; the axial thermal gradient is higher in the inlet region and increases with increasing values of E, NTU, R. The heat exchanger effectiveness e, defined as the ratio of the actual heat transfer rate(mc)p (Ti-- Tout), Tout=Tc(O), to the maximum hypothetical rateunder the same conditions (mc)min (Ti- νi), is shown in Figs. 6, 7respectively versus the number of transfer units and the flow capacitance ratio. As known, the balanced heat exchangers E = 1) present the worst behaviour ; the effectiveness does not depend on R and is the same for reciprocal values of the flow capacitance ratio.U形管换热器m . Spiga和g . Spiga,博洛尼亚摘要:分析解决方案提供一些两相流体在u形管换热器中的分布情况。
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Reading Material 2Shear Force And Bending Moment In BeamsLet us now consider,as an example ,a cantilever beam acted upon by an inclined load P at its free end [Fig.1.5(a)]. If we cut through the beam at a cross section mn and isolate the left-hand part of the beam as free body [Fig.1.5(b)] ,we see that the action of the removed part of the beam (that is ,the right-hand part) upon the left-hand part must be such as to hold the left-hand part in equilibrium. The distribution of stresses over the cross section mn is not known at this stage in our study ,but we do know that the resultant of these stresses must be such as to equilibrate the load P.It is convenient to resolve the resultant into an axial force N acting normal to the cross section and passing through the centroid of the cross section,a shear force V acting parallel to the cross section, and a bending moment M acting in the plane of the beam.The axial force ,shear force, and bending moment acting a across section of a beam are known as stress resultants. For a statically determinate beam,the stress resultants can be determined from equations of equilibrium. Thus ,for the cantilever beam pictured in Fig.1.5,we may write three equations of statics for the free-body diagram shown in the second part of the figure. From summations of force in the horizontal and vertical directions we find ,respectively,N=P cosβV=P sinβN=P cosβV=P sinβAnd,from a summation of moments about an axis through the centroid of cross sectionmn ,we obtain:M=Px sinβWhere x is the distance from the free and to section mn,thus, through the use of a free-body diagram and equations of static equilibrium,we are able to calculate the stress resultants without difficulty. The stresses in the beam due to the axial force N acting alone have been discussed in the text of Unit.2;now we will see how to obtain the stresses associated with bending moment M and the shear force V.The stress resultants N,V and M will be assumed to be positive when they act in the directions shown in Fig.1.5(b).this sign convention is only useful,however ,when we are discussing the equilibrium of the left-hand part of the beam. If the right-hand part of the beam is considered, we will find that the stress resultants have the same magnitudes but opposite directions [see Fig.1.5(a)] . Therefore,we must recognize that the algebraic sign of a stress resultant does not depend upon its direction in space, such as to the left or to the right, but rather it depends upon its direction in space ,such as to the left or to the right, but rather it depends upon its direction with respect to the material against which it acts. To illustrate this fact, the sign conventions for N, V and M are repeated in FIig1.6, where the stress resultants are shown acting on an element of the beam.We see that a positive axial force is directed away from the surface upon which it acts(tension) , a positive shear force acts clockwise about the surface upon which it acts ,and a positive bending moment is one that compresses the upper part of the beam.ExampleA simple beam AB carries two loads,a concentrated force P and a couple M O ,acting as shown in Fig.1.7(a). Find the shear force and bending moment in the beam at cross sections located as follows; (a) a small distance to the left of the middle of the beam and (b) a small distance to the right of the middle of the beam.SolutionThe first step in the analysis of this beam is to find the reactions R A and R B .takingmoments about ends A and B gives two equations of equilibrium, from which we findR A =4P 3—L M O R B =4P + LM O Next ,the beam is cut at a cross section just to the middle, and a free-body diagram is drawn of either half of the beam. In this example we choose the left -hand half of the beam, and the corresponding diagram is shown in Fig.1.7(b) .The force P and the reaction R A appear in this diagram as also do the unknown shear force V and bending moment M, both of which are shown in their positive directions ,The couple M O does not appear in the figure because the beam is cut to the left of the point where M O is applied. A summation of forces in the vertical direction givesV= R A —P= —4P —LM O Which shows that the shear force is negative; hence ,it acts in the opposite direction to that assumed in Fig.1.7(b). Taking moments about an axis through the cross section where the beam is cut [Fig.1.7(b)] gives M =2L R A —4PL =8PL —2M O Depending upon the relative magnitudes of the terms in this equation, we see that the bending moment M may be either positive or negative.To obtain the stress resultants at a cross section just to the right of the middle, we cut the beam at that section and again draw an appropriate free-body diagram [Fig.1.7(c)] . The only difference between this diagram and the former one is that the couple M O now acts on the part of the beam to the left of the cut section. Again summing forces in the vertical direction, and also taking moments about an axis through the cut section,we obtainV=—4P —L M O M = 8PL +2M OWe see from these results that the shear force does not change when the cut section is shifted from left to right of the couple MO,but the bending moment increase algebraically by an amount equalto MO.阅读材料2横梁的剪切力和弯矩现在让我们细想，例如，图1.5（a）所示的悬臂梁的自由端受到一个倾斜的载荷P的作用。